US3989598A - Antibiotic daunorubicin and its preparation - Google Patents
Antibiotic daunorubicin and its preparation Download PDFInfo
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- US3989598A US3989598A US04/777,876 US77787668A US3989598A US 3989598 A US3989598 A US 3989598A US 77787668 A US77787668 A US 77787668A US 3989598 A US3989598 A US 3989598A
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- daunorubicin
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
- C07H15/00—Compounds containing hydrocarbon or substituted hydrocarbon radicals directly attached to hetero atoms of saccharide radicals
- C07H15/20—Carbocyclic rings
- C07H15/24—Condensed ring systems having three or more rings
- C07H15/252—Naphthacene radicals, e.g. daunomycins, adriamycins
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
- C07H15/00—Compounds containing hydrocarbon or substituted hydrocarbon radicals directly attached to hetero atoms of saccharide radicals
- C07H15/20—Carbocyclic rings
- C07H15/22—Cyclohexane rings, substituted by nitrogen atoms
- C07H15/238—Cyclohexane rings substituted by two guanidine radicals, e.g. streptomycins
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S435/00—Chemistry: molecular biology and microbiology
- Y10S435/8215—Microorganisms
- Y10S435/822—Microorganisms using bacteria or actinomycetales
- Y10S435/886—Streptomyces
Definitions
- This invention relates to antibiotics and their preparation.
- the present invention provides the new antibiotic mixture hereinafter designated 9865 RP, and its three constituents, hereinafter designated 13057 RP, 13213 RP and 13330 RP.
- the constituent antibiotic 13057 RP which is known by the generic name daunorubicin and is also called rubidomycin or daunomycin, has proved to be of utility in treating certain tumours, namely lymphosarcoma, nephroblastoma, neuroblastoma, acute lymphoblastic leukemia and acute myeloblastic leukemia.
- the new antibiotic mixture 9865 RP is produced by the culture of two microorganisms, hereinafter more completely characterised, belonging to the genus Streptomyces and designated, respectively, Streptomyces 8899 and Streptomyces 31723.
- FIG. I is the ultra-violet spectrum of 9865 RP
- FIG. II is the infra-red spectrum of 9865 RP
- FIGS. III, V, VII and IX are the ultra-violet spectra of 13057 RP daunorubicin, the hydrochloride of 13057 RP daunorubicin, 13213 RP and the aglycone of 9865 RP, respectively, and FIGS.
- IV, VI, VIII and X are the infra-red spectra of 13057 RP daunorubicin, the hydrochloride of 13057 RP daunorubicin, 13213 RP, and the aglycone of 9865 RP, respectively.
- the constituents of 9865 RP can be detected by paper chromatography.
- the antibiotic is chromatographed on Arches No.302 paper impregnated with a pH 4.8 phosphate buffer, with n-butanol saturated with water, using descending development.
- the chromatogram is developed by bioautography on nutritive agar plates seeded with Bacillus subtilis or Klebsiella pneumoniae.
- the chromatogram shows that 9865 RP contains three active substances, herein named 13057 RP daunorubicin, 13215 RP and 13330 RP, the Rf value of which are, in this system, respectively 0.3, 0.7 and 0.9.
- 13057 RP daunorubicin is a base which forms acid addition salts.
- the aglycone of 9865 RP, 13057 RP daunorubicin and 13213 RP may be identified by circular paper chromatography, which is effected on Arches No.302 paper impregnated with a solution of acetone containing 20% formamide, with a 2:1 mixture of chloroform and benzene saturated with formamide. It is thus possible to demonstrate the existence of a single substance, having an Rf value of 0.86.
- the bacteriostatic activity of 9865 RP and of 13057 RP daunorubicin and 13213 RP, in relation to a certain number of organisms, has been determined by the dilution methods currently employed for this purpose. For each organism, the lowest concentration of substance has been determined which, under the defined condition, prevents all visible development in an appropriate nutritive broth. The results of various determinations are shown in Table VI, wherein the minimal bacteriostatic concentrations are expressed as micrograms of substance per cubic centimeter of experimental medium.
- the anticancer activities of 9865 RP and of its three constituents have been demonstrated in the laboratory, where they have been shown to be particularly active against transplantable tumours in the mouse, such as Ehrlich's ascitic tumour, sarcoma 180, benzopyrene saroma and lymphoblastic leucaemia AKR.
- the microorganisms which produce 9865 RP belong to the genus Streptomyces and are designated herein Streptomyces 8899 and Streptomyces 31723 respectively. They have been deposited at the Northern Regional Reseach Laboratory of Peoria, Ill., under the respective references NRRL 3046 and NRRL 3045. Subcultures of either of the said microorganisms can be obtained from the said depository by anyone freely and without restriction. The microorganisms were isolated from soil samples taken in two different regions of Norway.
- the method of isolation was as follows. The soil sample is suspended in sterile distilled water and the suspension diluted to various concentrations. A small volume of each dilution is spread on the surface of Petri dishes containing a nutritive agar medium. After incubation for several days at 26° C. the colonies of microorganisms which it is wished to isolate are pricked out onto agar slopes to give more abundant cultures.
- the sporulation of Streptomyces 8899 and 31723 is difficult to observe because of its complexity. It is observable either on "synthetic" media such as that described by Grundy et coll. (Antibiotics and Chemotherapy, 1, 309 (1951)) or on complex media such as Benett's medium (K. L. Jones, J. Bacteriol., 57, 142 (1949)). Cultures on thin plates examined under the microscope show the formation of branched filaments and of spore chains characteristic of the genus Streptomyces. The spore-bearing filaments presenting the most complex degree of development are in the form of spirals with serrated coils of several, and often more than five, turns. The spores are oval, measuring about 0.6 - 0.9 to 0.8 - 1.2 ⁇ .
- the attachment of the spore-bearing filaments presents a verticillated structure, sometimes monoverticillated but more often biverticillated. This structure is only observable under the microscope if the spore-bearing filaments are only spirals of one or two turns or are reduced to a loop; otherwise the development of spirals is too thick and masks their attachment, hindering the observation of any secondary whorls in their structures.
- Streptomyces 8899 and 31723 are placed in the Biverticillus-spira blue series section, in which no species are described, though Streptomyces coeruleorubidus appears in the Spira blue series section.
- Streptomyces 8899 and 31723 generally possess a vegetative mycelium which is usually rose or orange-rose at the beginning of development, the red colour intensifying with the incubation, becoming also bright red.
- organic media the vegetative cycelium is yellow-brown or red-brown.
- the aerial mycelium is generally well-developed on both types of medium. It is white at the beginning of its development and then rapidly becomes a shade of light blue, called below turquoise blue. According to the degree of development or the nature of the medium, it presents a slightly variable intensity of tone, or its colour may be slightly softened.
- Red or orange-red soluble pigments are formed in synthetic media of intensity which varies with the age of the cultures; the pigment is a softened red (red-brown or rose-brown) in organic media. On Williams and McCoy medium, an abundant production of characteristic black melanic pigment is observed.
- the cultures are carried out on agar slopes at 26° C.
- substances regularly giving rise to a rapid and complete growth are: xylose, arabinose, rhamnose, glucose, galactose, mannose, lactose, maltose, raffinose, dextrin, starch, glycerol (in S. 8899 only), adonitol, mannitol, sorbitol, inositol (in S. 8899 only).
- sorbose, inulin in S. 31723 only
- esculin erythritol and dulcitol allow no development, or only very restricted development.
- substances which produce an irregular, moderate or weak growth in the experiments include ribose, levulose, sucrose, inulin (in S. 8899 only), glycerol (in S. 31723 only), and inositol (in S. 31723 only).
- the characteristics to be taken into consideration for the systematic classification of S. coeruleorubidus strains 8899 and 31723 are: the turquoise blue colour of the aerial mycelium; the biverticillate structure of the spirals of the spore-bearing apparatus; the positive melamine reaction of cultures on appropriate media; the particular red colour of the vegetative mycelium on appropriate media; and the particular red colour of soluble pigments on appropriate media.
- S. coeruleorubidus strains 8899 and 31723 in the biverticillus-spira blue series section of Pridham's classification, in which no other species is described.
- the properties taken together place S. coeruleorubidus strains 8899 and 31723, in the new classification of S. A. Waksman "The Actinomycetes” (The Williams and Wilkins Company, Baltimore, 1961), Vol. II, page 155, in the melamine + group, series 5 (red to reddish-orange growth); no species occurs in this series having a blue aerial mycelium.
- S. coeruleorubidus strains 8899 and 31723 may therefore be placed in this series with the qualification "blue aerial mycelium".
- the process of the invention for the production of antibiotic 9865 RP comprises cultivating Streptomyces 8899 or Streptomyces 31723 or a productive mutant thereof in a nutrient medium containing assimilable sources of carbon, nitrogen, and mineral salts until substantial antibiotic activity is produced by the said microorganism in the said medium, and recovering the said antibiotic from the medium.
- the culture of Streptomyces 8899 or Streptomyces 31723 may be carried out by any method of aerobic surface or submerged culture, but the latter is preferred for reasons of convenience. For this purpose the various types of apparatus currently used in the fermentaion industry are employed.
- the fermentation medium must contain assimilable sources of carbon, nitrogen, and mineral salts and, optionally, growth factors, all these elements being introduced in the form of well-defined substances or as complex mixtures, such as those encountered in biological products of various origins.
- Carbohydrates such as glucose, lactose, sucrose, molasses; dextrins starch, and other carbohydrates such as the sugar alcohols, e.g. mannitol
- carbohydrates such as glucose, lactose, sucrose, molasses; dextrins starch, and other carbohydrates such as the sugar alcohols, e.g. mannitol
- certain organic acids e.g. lactic, citric, and tartaric acids.
- Certain animal or vegetable oils such as lard or soya oil may advantageously replace these various carbon sources, or be combined with them.
- sources of assimilable nitrogen are suitable. They may be simple chemical substances such as nitrates, inorganic and organic ammonium salts, urea and amino acids.
- nitrgoen principally in the form of protein such as casein, lactalbumin, gluten and hydrolysates therof, soya-, groundnut-, and fish-meals, meat extracts, yeast, distillers' solubles and corn-steep.
- certain may exert a buffering or neutralising effect such as alkali metal or alkaline earth metal phosphates and calcium and magnesium carbonates.
- Other mineral salts contribute to the ionic equilibrium necessary for the development of Streptomyces 8899 and 31723 and the formation of the antibiotic, for example alkali metal and alkaline earth metal chlorides and sulphates.
- certain substances act as activators of the metabolic reaction of Streptomyces 8899 and 31723; these are the salts of zinc, cobalt, iron, copper and manganese.
- the pH of the nutrient medium at the beginning of culture should be between 6.0 and 7.8, and preferably 6.5 to 7.5.
- the optimal temperature for the culture is 25°-28° C., but satisfactory production is obtained at temperatures between 23° and 35° C.
- the aeration of the fermentation medium may b varied over a fairly wide range of values but it has been found that aeration rates of 0.3 to 2 liters of air per minutes per liter of medium are particularly suitable.
- the maximal yield of antibiotic is obtained after 2 to 5 days of culture, this period depending essentially on the medium used. From the foregoing it will be appreciated that the general conditions for the culture of Streptomyces 8899 and 31723 for the production of antibiotic 9865 RP may be varied to a fairly wide degree.
- 9865 RP may be isolated from the fermentation cultures by various methods.
- the fermentation culture may be filtered at a pH between 1.5 and 9 and, in these conditions, the major part of the active material passes into the filtrate. After washing with water, the filter-cake retains practically no active material. It is advantageous to carry out this operation using an acid medium, and particularly one acidified with oxalic acid to a pH between 1.5 and 2. It is also possible to carry out the filtration at a pH between 2 and 7, preferably near to 2, in the presence of an aliphatic alcohol containing 1 to 3 carbon atoms.
- 9865 RP is obtained in aqueous or aqueous-alcoholic solution and it is then extracted with a water-immiscible organic solvent such as butanol, methyl isobutyl ketone, ethyl acetate or chloroform, at a pH between 5.5 and 9, preferably about 7.5.
- a water-immiscible organic solvent such as butanol, methyl isobutyl ketone, ethyl acetate or chloroform
- This extraction may be preceded by absorption of the antibiotic on an ion-exchange resin, in which case the aqueous solution is adjusted to a pH about 4 and then treated with a cationic carboxylic exchange resin, preferably Amberlite IRC 50, in the hydrogen form.
- Elution is then effected with a saline or acidic, aqueous-alcoholic solution, preferably with methanol containing 10% water and 1% sodium chloride.
- the eluate is concentrated to remove the alcohol and then
- the fermentation medium may also be directly extracted with a water-immiscible organic solvent such as butanol, ethyl acetate or chloroform, at a pH between 5.5 and 9, preferably about 7.5.
- a water-immiscible organic solvent such as butanol, ethyl acetate or chloroform
- the antibiotic 9865 RP is finally obtained in organic solution. It may be advantageous at this stage to purify the antibiotic by successively passing it into aqueous solution and into organic solution by varying the pH.
- the crude antibiotic may then be isolated from the organic solution obtained in the last-mentioned operation by concentration or precipitation with a poor solvent for the antibiotic, such as hexane.
- a method of isolation which has been found to be particularly advantageous consists of acidifying the organic solution to a pH of about 4, preferably with acetic acid, and concentrating it under reduced pressure to a smaller volume. Addition of a poor solvent for 9865 RP, such as hexane, to the concentrate obtained causes the precipitation of the crude antibiotic.
- the 9865 RP isolated by any of the foregoing methods may then be separated into its three constituents, 13057 RP daunorubicin, 13213 RP and 13330 RP.
- This separation may be effected by the usual methods used for the separation of an antibiotic into its constituents, such as chromatography on various substances or countercurrent distribution.
- the various countercurrent distribution operations may be preceded or followed by the usual purification processes, particularly extraction or recrystallisation, in order to obtain the three constituents in a form pure enough for the use envisaged.
- Activity is throughout determined by turbidimetric estimation, using Klebsiella pneumoniae as the sensitive organism, by comparison with a sample of 9865 RP of known activity used as control. This activity is expressed in units (u) per mg. for solid products and in units per cc. for solution. (The unit is defined as the smallest quantity of product which, dissolved in 1 cc. of an appropriate medium, inhibits the growth of Klebsiella pneumoniae under the conditions in question).
- a 170 liter fermentation vessel is charged with:
- This culture medium has a pH of 6.15. It is sterilised by passage of steam at 122° C. for 40 minutes. After cooling, the volume of the broth is 120 liters and the pH is 7.20. The medium is then seeded with 200 cc. of a culture in an agitated Erlenmeyer flask of the strain Streptomyces 31723. The culture is carried out for 27 hours at 26°-27° C. with agitation and aeration with sterile air. It is then suitable for seeding the production culture.
- the production culture is carried out in an 800 liter formentation vessel charged with the following:
- the pH of the medium thus obtained is adjusted to 7.20 with concentrated sodium hydroxide solution (400 cc.).
- the medium is then sterilised by the passage of steam at 122° C. for 40 minutes. After cooling, the volume of the broth is 500 liters and the pH is 6.75. It is then seeded with 50 liters of the culture from the 170 liter fermentation vessel. Culture is carried out at 28° C. for 67 hours with agitation and aeration with sterile air.
- the pH of the medium is then 7.40 and the volume of the fermentation culture is 520 liters.
- the quantitiy of antibiotic present in the medium is 29 ⁇ /cc.
- An inoculum culture is carried out in a 170 liter fermentation vessel under the same conditions as in Example 1 but seeding with 200 cc. of a culture in an agitated Erlenmeyer flask of the strain Streptomyces 8899.
- the production culture is then carried out in an 800 liter fermentation vessel charged with the medium described in Example 1.
- the pH of the medium is adjusted to 8.10 with concentrated sodium hydroxide solution (750 cc.), and the medium is then sterilised by the passage of steam at 122° C. for 40 minutes. After cooling, the volume of the broth is 500 liters and the pH 6.80.
- the medium is then seeded with 75 liters of the culture in the 170 liter fermentation vessel, and the culture is carried out at 26°-27° C. for 67 hours with agitation and aeration with sterile air.
- the pH of the medium is then 7.40 and the volume of the fermentation culture is 545 liters.
- the quantity of antibiotic present in the medium is 9.1 ⁇ /cc.
- Example 1 The fermentation culture from Example 1 (520 liters: activity 29 ⁇ /cc.) is placed in a vessel equipped with an agitator and the pH is adjusted to 1.8 with a concentrated solution of oxalic acid. Agitation is carried out for one hour and a filtration adjuvant (20 kg.) then added. The mixture is filtered on a filter-press and the filter-cake washed with water (100 liters) acidified to pH 2 with oxalic acid. The filtrate (612 liters) is treated with concentrated sodium hydroxide solution until the pH is 4.5.
- the filtrate is then passed through a column containing Amberlite IRC 50 in hydrogen form (20 liters: diameter of column 15.2 cm., height of column 200 cm., height of resin at rest in column 110 cm.).
- the filtrate passes through the bed of Amberlite from base to top at a rate of 40 liters/hour.
- the column is then washed with water (100 liters) at a rate of 50 liters/hour circulating from base to top and then with methanol (containing 10% water; 75 liters) circulating from top to base at a rate of 50 liters/hour.
- the washings are discarded and the column is then eluted with a solution having the following composition (per liter):
- the eluate (100 liters), which contains the major part of the antibiotic, is concentrated under reduced pressure at 35° C. to 10 liters.
- the concentrate is extracted at pH 7.5 with chloroform (2 ⁇ 5 liters).
- the chloroformic extract is adjusted to pH 4 with a solution of acetic acid in chloroform (10:100 by volume) and then concentrated at 30° C. under reduced pressure to 100 cc.
- the antibiotic is precipitated by the addition of hexane (1 liter), separated, washed and dried to give an amorphous red powder (9 g.) of activity 1,400 ⁇ /mg.
- the crude antibiotic (17.1 g.) obtained as described in Example 3 (activity 1530 ⁇ /mg.) is dissolved with stirring in a mixture of methylene chloride (1.5 liters), carbon tetrachloride (0.3 liters) and water (1.8 liters). The pH is then adjusted to 3 by the addition of normal hydrochloric acid (8 cc.). After decanting, the aqueous phase is treated with methylene chloride (7 liters) and 0.1N sodium hydroxide solution (200 cc.) to give a pH of 7.5. After decanting, the aqueous phase is again extracted at pH 7.5 with methylene chloride (3.5 liters). The methylene chloride extracts are combined and concentrated to 100 cc.
- a mixture is prepared of methylene chloride, carbon tetrachloride and MacIlvaine buffer - pH 5.8 (20 cc. of this buffer are prepared by the addition of 12.09 cc. of 0.2 M Na 2 HPO 4 solution to 7.91 cc. of 0.1 M citric acid solution) in the proportions 2:1:3 (by volume). When this mixture is in equilibrium, the two phases are separated. 9865 RP (10 g.) of activity 1750 ⁇ /mg. (obtained as described in Example 4) is dissolved in a mixture of the phases (1 liter of each).
- This system is subjected to a countercurrent distribution of 6 transfers in 5 liter cells, using the heavy (organic solvent) phase as the mobile phase and the light (aqueous) phase as the stationary phase and using 1 liter of each phase each time.
- the mixtures of lower phases (mixture A) and upper phases (mixture B) of the first 4 cells, and the mixtures of lower phases (mixture C) and upper phases (mixture D) of the last 3 cells, are collected separately.
- Mixture B is adjusted to pH 7.5 by the addition of normal sodium hydroxide solution (300 cc.) and then extracted with chloroform (4 liters, 2 liters and 1 liter).
- the chloroformic extracts and mixture A are combined and concentrated under reduced pressure (to 700 cc.).
- the concentrate is washed with water at pH 7.5 (2 ⁇ 350 cc.) and the mother liquors of the washings are extracted with chloroform (2 ⁇ 100 cc.).
- the washed concentrate and the chloroformic extracts are combined and concentrated under reduced pressure to 70 cc.
- mixture D is extracted with methylene chloride (3 liters and 1.5 liters).
- the methylene chloride extracts and mixture C are combined and concentrated under reduced pressure to 800 cc.
- the concentrate is washed with water (400 cc.) and then concentrated again to 700 cc.
- Hexane (1 liter) is added and the precipitate produced is filtered off, washed and dried under reduced pressure at 30° C., to give a fraction F 2 (3.7 g.) containing principally 13213 RP and 13330 RP.
- the mixture of the upper phases of cells 0 to 37 (3.8 liters) is recovered and concentrated to 300 cc.)
- the concentrate thus obtained and the mixture of the lower phases of cells 0 to 37 (3.8 liters) are then combined and concentrated to 800 cc.
- the pH is adjusted to 8 by the addition of normal sodium hydroxide solution (180 cc.) and the solution obtained is extracted with chloroform (800 cc. and 400 cc.).
- the chloroformic extracts are concentrated to 400 cc. and washed with water (400 cc.) made alkaline to pH 8.
- the mother liquors of the washing are extracted with chloroform (200 cc.).
- the washed concentrate and the chloroformic extracts are combined, concentrated to 400 cc., washed with water (400 cc.) made alkaline to pH 8, and concentrated to 100 cc. Butanol (200 cc.) is added, and the mixture concentrated to 100 cc.
- the butanolic solution obtained is adjusted to pH 3.5 by the addition of butanol saturated with normal hydrochloric acid (30 cc.) and kept for 12 hours at 4° C. Crystals form which are filtered off, washed and dried, giving a first crop (4.55 g.) of crude 13057 RP daunorubicin hydrochloride. Concentration to 100 cc. of the crystallisation mother liquors, addition of hexane (1 liter) and filtering, washing and drying the precipitate produced, gives a second crop (2.5 g.) of crude 13057 RP daunorubicin hydrochloride.
- This compound (0.208 g.) is dissolved in a mixture of water (200 cc.) and butanol (150 cc.). 0.1N sodium hydroxide solution (3.4 cc.) is added, the mixture is separated and the aqueous phase then extracted with butanol (50 cc.). The butanolic extracts are combined, washed with water made alkaline to pH 8 (2 ⁇ 100 cc.) and concentrated to 10 cc.
- the concentrate obtained is treated with hexane (50 cc.) and the precipitate producted is filtered off, washed and dried, giving 13057 RP daunorubicin (0.0945 g.) in the form of an amorphous red powder, activity 160 ⁇ /mg.
- the mixture of the upper phases of cells 36 to 89 (5.3 liters) is recovered and concentrated to 500 cc.
- the concentrate thus obtained and the mixture of the lower phases of cells 36 to 89 (5.3 liters) are combined and concentrated to 800 cc.
- the concentrate is extracted successively with methylene chloride (2 ⁇ 800 cc.) and chloroform (800 cc.).
- the extracts obtained are combined, concentrated to 400 cc., washed with water at pH 7.5 (2 ⁇ 400 cc.) and then concentrated to 10 cc.
- Addition of hexane (100 cc.) causes the precipitation of a product which is filtered off, wahed and dried under reduced pressure, giving 13213 RP (1.1 g.) in the form of an amorphous orange-red powder, activity 2,650 ⁇ /mg.
- Example 2 The fermentation culture (500 liters) obtained in Example 2 is treated as described in Example 3, giving crude 9865 RP (8.5 g.), activity 395 ⁇ /gm.
- This crude product (17 g.) is purified as described in Example 4 but replacing the methylene chloride by ethyl acetate to give 9865 RP (3 g.), activity 1300 ⁇ /mg.
- 9865 RP (12.4 g.), obtained as described in Example 9, is subjected, in a butanol - pH 7.35 M/3 phosphate buffer system, to a 50-transfer countercurrent distribution.
- a first crop (1 g.) of 13057 RP daunorubicin hydrochloride is obtained, followed, after concentration of the mother liquors, by a second crop (1.1 g.) of the same product.
- These two crops, after recrystallisation from aqueous dioxan take the form of orange-red needles, m.p. about 225°-230° C. (with decomposition), activity 67 ⁇ /mg.
- a similar treatment applied to cells 36 to 49 gives crude 13213 RP (1.1 g.), activity 1800 ⁇ /mg., which, after being subjected to a 50-transfer countercurrent distribution in a butanol-ethyl acetate - pH 4 MacIlvaine buffer sytem (3:7:10 by volume), gives 13213 RP (0.5 g.) in the form of an amorphous orange-red powder, activity 2000 ⁇ /mg.
- a fermentation culture (625 liters), prepared as described in Example 2, is placed in an agitated vessel.
- the pH is adjusted to 9 with concentrated sodium hydroxide solution. Agitation is continued for 30 minutes and a filter-adjuvant (32 kg.) then added.
- the mixture is filtered on a filter-press and washed with water (275 liters).
- the filtrate (780 liters) is treated with sodium chloride (156 kg.) and the pH adjusted to 3 with 12N hydrochloric acid.
- the filtrate is then extracted with butanol (260 liters) and the butanolic extract concentrated under reduced pressure at 35° C. to 4 liters.
- the concentrate is filtered and the crude antibiotic precipitated from the clarifed solution with petroleum ether (32 liters), separated, washed and dried in vacuo at 30° C., giving crude 9865 RP (227 g.) as a red-brown powder, activity 45 ⁇ /mg.
- the crude product (50 g.) obtained is dissolved in butanol saturated with water (200 cc.) and the solution obtained is chromatographed at pH 4 through a column containing alumina (500 cc.). After fixation of the antibiotic, the chromatogram is developed and eluted with butanol saturated with water (4 liters). Three coloured fractions are recovered (respective volumes 450 cc., 1500 cc. and 1500 cc.). The first fraction is concentrated under reduced pressure to 50 cc. and then treated with hexane (500 cc.), giving 9865 RP (8.3 g.), activity 68.5 ⁇ /mg. The second two fractions are each concentrated under reduced pressure to 100 cc. and treated with hexane (1 liter each) to give, respectively, 9865 RP (4.4 g.), activity 216 ⁇ /mg. and 9865 RP (1.35 g.), activity 800 ⁇ /mg.
- the filter-cake is washed with water (100 liters) acidified to pH 2 with oxalic acid and the combined filtrate obtained (500 liters) is extracted at pH 8 with chloroform (150 liters and 100 liters).
- the extracts are combined and extracted with water at pH 4 (80 liters and 50 liters).
- the aqueous extract obtained is made alkaline to pH 8 with normal sodium hydroxide solution and extracted with chloroform (40 liters and 20 liters).
- the chloroformic extracts thus obtained are acidified to pH 4 with a solution of acetic acid in chloroform (10:100 by volume) and the acidified extract concentrated at 30° C. under reduced pressure to 50 cc.
- the crude antiobiotic is then precipitated by the addition of hexane (500 cc.), separated, washed and dried in vacuo at 30° C., giving 9865 RP (680 mg.) in the form of a red powder, activity 1080 ⁇ /mg.
- 13057 RP daunorubicin (500 mg.), obtained as described in Example 7, is treated with sulphuric acid as described in Example 13 for 9865 RP, giving crystals (300 mg.) which, after being treated as described in Example 13, yield the aglycone of 13057 RP daunorubicin (202 mg.) in the form of orange-red needles having a first melting point at 160° C. and a second at 225°-230° C. This aglycone is identical with that of 9865 RP.
- compositions containing at least one of the antibiotics defined above is association with a compatible pharmacologically acceptable carrier.
- the compositions may also contain other physiologically active substances. These compositions may be made up in any pharmaceutical form appropriate for the route of administration in question. Intravenous administration of 13057 RP daunorubicin is preferred.
- Solid compositions for oral administration include compressed tablets, pills, dispersible powders, and granules.
- one or more of the new antibiotics is, or are, admixed with at least one inert diluent such as calcium carbonate, potato starch, alginic acid, or lactose.
- the compositions may also comprise, as in normal practice, additional substances other than inert diluents. e.g. lubricating agents, such as magnesium stearate.
- Liquid compositions for oral administration include pharmaceutically acceptable emulsions, solutions, suspensions, syrups and elixirs containing inert diluents commonly used in the art, such as water and liquid paraffin.
- compositions may also comprise adjuvants, such as wetting and suspending agents, and sweetening, flavouring, perfuming and preserving agents.
- adjuvants such as wetting and suspending agents, and sweetening, flavouring, perfuming and preserving agents.
- the compositions according to the invention, for oral administration also include capsules of absorbable material such as gelatin containing one or more of the new antibiotics with or without the addition of diluents or excipients.
- Preparations according to the invention for parenteral administration include sterile aqueous or non-aqueous solutions, suspensions, or emulsions.
- non-aqueous solvents or suspending media are propylene glycol, polyethylene glycol, vegetable oils such as olive oil, and injectable organic esters such as ethyl oleate.
- These compositions may also contain adjuvants such as preserving, wetting, emulsifying and dispersing agents. They may be sterilised by, for example, filtration through a bacteria-retaining filter, by incorporation in the compositions of sterilising agents, by irradiation, or by heating. They may also be manufactured in the form of sterile solid compositions, which can be dissolved in sterile water or some other sterile injectable medium immediately before use.
- compositions of the invention may be varied, it being necessary that it should constitute a proportion such that a suitable dosage for the therapeutic effect desired shall be obtained. Obviously several unit dosage forms may be administered at about the same time.
- the preparations should normally contain at least 0.001 % by weight of active substance when required for administration by injection.
- the preparations will normally contain at least 0.1 % by weight of active substance.
- compositions for injection consist, for example, of a solution containing 0.1 mg/cc. of active substance in sterile physiological saline.
- Daunorubicin is essentially intended to obtain a remission.
- the induction treatment, and the reinduction treatments which may follow it consist of injections repeated at progressively increasing intervals, spaced over from one to several months, which excludes the use of daunorubicin as a maintenance treatment by itself and for a prolonged period.
- Daunorubicin exercises a depressant action on the blood-forming centers and its administration is sometimes accompanied by cardiac complications. Daunorubicin cannot be used without frequent and regular blood tests and rigorous cardiological testing, before and during treatment.
- Daunorubicin is preferably administered by means of intravenous perfusion.
- Solutions of daunorubicin must be prepared at the time they are required. This is done, for example, by shaking together in a stoppered vessel 20 mg of dry daunorubicin and the contents of an ampoule (4 cc) of solvent (water for injectable preparations), until the daunorubicin is completely dissolved.
- the solution prepared in this manner is injected through a catheter as a venous perfusion in 100 or 200 cc of isotonic sodium chloride solution.
- the dosage varies according to the clinical circumstances, the therapeutic response, and the blood picture. Also, the data given hereafter indicate mainly an order of magnitude.
- Treatment of acute leukaemias must be intensive and of short duration; depending on the case, it comprises one or more courses.
- the actual trend is to administer a daily dose of 1 mg/kg body weight of two to eight consecutive days, and to cease injections when the leucopenia reaches 1,000 to 1,500 units per cc.
- characteristic changes in the medullary cytology fcilitate the conducting of the treatment and help in its adaptation to each particular case.
- the appearance of giant lymphoblasts slightly preceding aplasia indicates that administration of daunorubicin should be suspended.
- the overall dosage corresponding to the group of courses making up the initial treatment, such as has just been defined, is far from being uniform; calculated per kg weight, it sometimes reaches 20 mg, a dose of around 25 mg being considered the maximum safe dose.
- the procedure is identical in acute myeloblastic leukaemias, but the daily dose is increased to 2 mg/kg.
- Various schemes of multiple chemotherapy incorporating daunorubicin have been proposed.
- One such technique involves an initial treatment completed by a reinforcing therapy on which reinduction treatments are grafted.
- the initial treatment combines daily oral administration of prednisone and weekly intravenous injections, in the form of a perfusion, of daunorubicin and vincristine until complete remission is obtained.
- the doses are 100 mg per day of prednisone, 2 mg of vincristine and 60 mg of daunorubicin per week.
- a repeat injection of vincristine (2 mg/m 2 ) and daunorubicin (30 mg/m 2 ) is given; then the maintenance treatment is started, combining daily ingestion of 6-mercaptopurine (90 mg/m 2 ) and intramuscular administration, every 7 days, of methotrexate (15 mg/m 2 ).
- the reinduction treatments intended for the 2nd, 4th, 7th, 11 months, and so on, consist of a twice weekly injection of daunorubicin and vincristine in doses respectively of 30 mg/m 2 and 2 mg/m 2 per injection, as well as daily absorption of prednisone for 7 days.
- methotrexate is administered by spinal injection, at the rate of two injections during each reinduction and one monthly injection in between.
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Abstract
The invention provides the novel antibiotic known as daunorubicin (13057 RP) which has a powerful anti-cancer effect and is also an anti-bacterial agent. This antibiotic is a constituent of a mixture of three antibiotics, called 9865 R.P., produced by aerobic culture of one of the strains of Streptomyces, NRRL 3046 and 3045.
Description
This application is a continuation-in-part of our prior copending application Ser. No. 280,816, filed May 16, 1963.
This invention relates to antibiotics and their preparation.
The present invention provides the new antibiotic mixture hereinafter designated 9865 RP, and its three constituents, hereinafter designated 13057 RP, 13213 RP and 13330 RP.
9865 RP, and its three constituents, possess a very pronounced anticancer activity, they also possess a very important antibacterial effect both against Gram-positive and Gram-negative organisms. This property is all the more valuable in that they retain a high level of activity against organisms (and in particular staphylococcal strains) which have become resistant to antibiotics currently in use or to certain anticancer antibiotics, such as actinomycin and rufochromomycin.
The constituent antibiotic 13057 RP, which is known by the generic name daunorubicin and is also called rubidomycin or daunomycin, has proved to be of utility in treating certain tumours, namely lymphosarcoma, nephroblastoma, neuroblastoma, acute lymphoblastic leukemia and acute myeloblastic leukemia.
The new antibiotic mixture 9865 RP is produced by the culture of two microorganisms, hereinafter more completely characterised, belonging to the genus Streptomyces and designated, respectively, Streptomyces 8899 and Streptomyces 31723.
The antibiotic mixture 9865 RP has the following characteristics: it is an amorphous orange-red powder soluble in chlorinated solvents, such as chloroform and dichloroethane, moderately soluble in water acidified to between pH 3 and 4, very slightly soluble in alcohols and practically insoluble in water, benzene and diethyl ether; it contains carbon, hydrogen, oxygen and nitrogen in the following proportions as determined by analysis, C = 61.0%, H = 6.2%, O = 28.15%, M = 2.65%, its ultra-violet spectrum (as determined on a solution in 96% ethanol) shows absorption maxima at 236 mμ, E1 cm.1% = 425, 255 mμ, E1 cm.1% = 308, 290 mμ, E1 cm.1% = 114, and 495 mμ, E1 cm.1% = 146, and absorption minima at 245 mμ, E1 cm.1% = 284, 280 mμ, E1 cm.1% = 108, and 325 mμ, E1 cm.1% = 20, and a shoulder at 533 mμ, E1 cm.1% = 80; its infra-red spectrum (as determined on tablets made up with potassium bromide) shows the following principal absorption bands;
TABLE I
______________________________________
about 3450 S 1147 sh
2925 S 1113 S
1715 S 1080 S
1615 S 1067 S
1580 S 1030 S
1445 S 1005 vS
1410 vS 990 vS
1377 S about 945 sh
1350 S 917 m
1282 vS 873 m
1260 sh 840 m
1230 S 815 m
1205 vS 793 m
about 1190 sh 764 m
about 690 m
______________________________________
vS = very strong
S = strong
m = medium
sh = shoulder.
The accompanying drawings show the ultra-violet and infra-red absorption spectra of 9865 RP and its three constituents. In the drawings, FIG. I is the ultra-violet spectrum of 9865 RP and FIG. II is the infra-red spectrum of 9865 RP. FIGS. III, V, VII and IX are the ultra-violet spectra of 13057 RP daunorubicin, the hydrochloride of 13057 RP daunorubicin, 13213 RP and the aglycone of 9865 RP, respectively, and FIGS. IV, VI, VIII and X are the infra-red spectra of 13057 RP daunorubicin, the hydrochloride of 13057 RP daunorubicin, 13213 RP, and the aglycone of 9865 RP, respectively.
The constituents of 9865 RP can be detected by paper chromatography. The antibiotic is chromatographed on Arches No.302 paper impregnated with a pH 4.8 phosphate buffer, with n-butanol saturated with water, using descending development. The chromatogram is developed by bioautography on nutritive agar plates seeded with Bacillus subtilis or Klebsiella pneumoniae. The chromatogram shows that 9865 RP contains three active substances, herein named 13057 RP daunorubicin, 13215 RP and 13330 RP, the Rf value of which are, in this system, respectively 0.3, 0.7 and 0.9.
These three constituents, of which 13057 RP daunorubicin is particularly important, may be isolated from 9865 RP, by various methods, some of which will be described below. 13057 RP daunorubicin is a base which forms acid addition salts. The free base is an amorphous red powder soluble in alcohols and chloroform, very slighly soluble in water and ketones and practically insoluble in benzene and diethyl ether; it contains carbon,, hydrogen, oxygen and nitrogen in the following proportions, as determined by analysis, C = 59.8%, H = 5.85%, N = 2.3%, O = 29.45%; it melts at 155°-170° C. (with decomposition); its ultra-violet spectrum (as determined on a solution in 96% ethanol) shows absorption maxima at 236 mμ, E1 cm.1% = 621, 255 mμ, E1 cm.1% = 426, 290-295 mμ, E1 cm.1% = 135, and 482-498 mμ, E1 cm.1% = 230, and absorption minima at 245 mμ, E1 cm.1% = 378, 280 mμ, E1 cm.1% = 122, and 325 mμ, E1 cm.1% = 10, and a shoulder at 533 mμ, E1 cm.1% = 127; its infra-red spectrum (as determined on tablets in mixture with potassium bromide) shows the following principal absorption bands:
TABLE II
______________________________________
about 3450
vS 1410 S 1205 S 1068 m
2925 S 1380 S about 1190
sh 1033 m
1715 m 1355 S 1150 sh 1010 S
1615 S 1282 S 1117 S 983 S
1582 S 1262 sh 1090 m 950 w
1447 S 1230 S 1080 m 918 w
867 w 815 m 790 m 762 m
about 840 w
______________________________________
vS = very strong
S = strong
m = medium
w = weak
sh = shoulder;
it hydrochloride forms orange-red needles soluble in water and alcohols, slightly soluble in chloroform and practically insoluble in benzene and diethyl ether, has the following elemental composition as determined by analysis; C = 55.4%, H = 5.45%, O = 28.8%, N = 2.13%, Cl = 6.15%, melts at 225°-230° C. (with decomposition), shows the optical rotation [α]D 20 = + 240° (c = 0.1; methanol), has an ultra-violet spectrum (as determined on a solution in 96% ethanol) showing absorption maxima at 236 mμ, E1 cm.1% = 594, 255 mμ, E1 cm.1% = 410, 290-295 mμ, E1 cm.1% = 129, and 482-498 mμ, E1 cm.1% = 218, and absorption minima at 245 mμ,, E1 cm.1% = 360, 280 mμ , E1 cm.1% = 118, and 325 mμ, E1 cm.1% = 10, and a shoulder at 533 mμ, E1 cm.1% = 120, and has an infra-red spectrum (as determined on tablets in mixture with potassium bromide) showing the following principal absorption bands:
TABLE III
______________________________________
about 3450
vS 1350 S 1080 S 882 m
about 2925
S 1282 vS 1064 S 867 S
1707 S 1260 sh 1028 S 838 S
1610 vS 1228 S 1000 vS 813 S
1575 vS 1205 vS 982 vS 788 S
1439 vS about 1190
sh 950 m 762 S
1408 vS about 1145
sh 935 m about 692
m
1370 S 1112 vS 912 m
______________________________________
vS = very strong
S = strong
m 32 medium
sh = shoulder.
13213 RP is an amorphous orange-red powder soluble in chlorinated solvents, such as chloroform, and in dimethylformamide, moderately soluble in water acidified to between pH 3 to 4, very slightly soluble in alcohols and practically insoluble in water, benzene and diethyl ether; it contains carbon, hydrogen and nitrogen in the following proportions, as determined by analysis, C = 58.6%, H = 6.2%, N = 2.2%, and also contains oxygen; it has an ultra-violet spectrum (as determined on a solution in 96% ethanol) showing absorption maxima at 236 mμ, E1 cm.1% = 425, 255 mμ, E1 cm.1% = 297, 290-295 mμ, E1 cm.1% = 108, and 480-495 mμ, E1 cm.1% = 155, and absorption minima at 245 mμ, E1 cm.1% = 274, 280 mμ, E1 cm.1% = 103, and 325 mμ, E1 cm.1% = 20, and a shoulder at 533 mμ, E1 cm.1% = 90; and its infra-red spectrum (as determined on tablets in mixture with potassium bromide) shows the following principal absorption bands:
TABLE IV
______________________________________
about 3450
S 1377 S about 1190
sh 995 S
about 2925
m 1352 S about 1180
sh about 837
m
1715 m 1282 S 1117 vS 812 S
1615 S 1262 S about 1080
S about 796
S
1583 S 1230 S 1032 S 765 m
about 1445
S 1205 S 1008 S about 690
m
1412 S
______________________________________
vS = very strong
S = strong
m = medium
sh = shoulder.
The acid hydrolysis of 9865 RP and of its two main constituents, 13057 RP daunorubicin and 13213 RP, liberates amino-sugars and a coloured substance which is an aglycone. This aglycone forms orange-red needles, soluble in alcohols, ethyl acetate an chloroform, slightly soluble in benzene and diethyl ether, and insoluble in water; it has the following composition as determined by analysis: C = 63.4%, H = 5.7%, O = 30.4%, N = less than 0.2%; it melts at 160° C, and again at 225°-230° C.; its ultra-violet spectrum (as determined on a solution in 96% ethanol) shows absorption maxima at 236 mμ, E1 cm.1% = 835, 255 mμ, E1 cm.1% = 570, 290-295 mμ, E1 cm.1% = 167, and 470-495 mμ, E1 cm.1% = 272, and absorption minima at 245 mμ, E1 cm.1% = 510, 280 mμ, E1 cm.1% = 149, and 325 mμ, E1 cm.1% = about 0, and a shoulder at 533 mμ, E1 cm.1% = 145; its infra-red spectrum (as determined on tablets in mixture with potassium bromide) shows the followig principal absorption bands:
TABLE V
______________________________________
about 3430
S 1350 S about 1083
S 835 S
about 2910
S 1275 vS 1065 S 808 S
1707 S 1228 vS 1032 S 790 S
1610 vS 1210 vS 988 vS 762 S
1575 vS 1185 sh 941 m 737 m
1440 vS 1150 m 918 m 718 m
1415 vS 1117 S 858 m 695 S
1375 vS
______________________________________
vS = very strong
S = strong
m = medium
sh = shoulder.
The aglycone of 9865 RP, 13057 RP daunorubicin and 13213 RP may be identified by circular paper chromatography, which is effected on Arches No.302 paper impregnated with a solution of acetone containing 20% formamide, with a 2:1 mixture of chloroform and benzene saturated with formamide. It is thus possible to demonstrate the existence of a single substance, having an Rf value of 0.86.
The bacteriostatic activity of 9865 RP and of 13057 RP daunorubicin and 13213 RP, in relation to a certain number of organisms, has been determined by the dilution methods currently employed for this purpose. For each organism, the lowest concentration of substance has been determined which, under the defined condition, prevents all visible development in an appropriate nutritive broth. The results of various determinations are shown in Table VI, wherein the minimal bacteriostatic concentrations are expressed as micrograms of substance per cubic centimeter of experimental medium.
TABLE VI
__________________________________________________________________________
ANTIBACTERIAL SPECTRA
__________________________________________________________________________
13057 RP
9865 RP daunorubicin
13213 RP
Minimal Minimal Minimal
bacteriostatic
bacteriostatic
bacteriostatic
concentration
concentration
concentration
Bacterial strains tested
mcg./cc.
mcg./cc.
mcg./cc.
__________________________________________________________________________
Staphylococcus aureus,
strain 209 P - ATCC 6538 P
0.20 4.3 0.14
" Oxford strain - ATCC 9144
0.26 4.2 0.15
" strain 133 (Institut Pasteur)
0.14 4.2 0.083
" strain B.sub.3 (streptomycin and
0.35 5.2 0.20
penicillin resistant)
" strain Hb (tetracycline and
0.32 5.3 0.17
penicillin resistant)
" strain Launoy 1 (tetracycline,
0.21 7.1 0.091
streptomycin, chloramphenicol and
penicillin resistant)
" strain Launoy 2 (tetracycline,
0.17 4.8 0.091
streptomycin and penicillin
resistant)
" strain Beaujon 3 (tetracycline,
0.16 4.4 0.068
streptomycin, chloramphenicol and
penicillin resistant)
" strain 2700 R (streptothricin
0.21 4.7 0.10
resistant)
" strain 1142 R (congocidin resistant)
0.17 2.1 0.10
" strain 3486 R (spiramycin resistant)
0.21 5.2 0.091
" carbomycin resistant strain
0.23 5.3 0.12
" erythromycin resistant strain
0.11 3.8 0.055
" chloramphenicol resistant strain
0.08 4.1 0.045
" novobiocin resistant strain
0.12 3.9 0.075
" streptogramin resistant strain
0.16 1.9 0.076
" actinomycin resistant strain
0.19 5.8 0.10
" strain 662 R (rufochromomycin
0.29 6.3 0.16
resistant)
Micrococcus citreus- ATCC 8,411 0.71 4.2 0.19
Micrococcus lysodeikticus 0.21 2.5 0.068
Gaffkya tetragena (Fac.Phie) 0.44 6.7 0.23
Sarcina lutea - ATCC 9341 0.15 1.2 0.088
Sarcina alba (Fac.Phie) 0.38 3.3 0.18
Streptococcus faecalis
(Thiercelin's enterococcus
1.2 19 0.55
Fac.Phie)
"
ATCC 9790 2.1 30 1
Streptococcus viridans
(Institut Pasteur) 43 2.1
Streptococcus pyogenes
Hemolyticus (strain Dig 7,
0.11 1.6 0.17
Instut Pasteur)
Diplococcus pneumoniae (strain Til. Institut Pasteur)
0.075 0.89 0.05
Neisseria catarrhalis (Fac.Phie)
0.31 2.2 0.12
Corynebacterium pseudodiphtericum (Fac.Phie)
0.026 1.7 0.017
Lactobacillus casei - ATCC 7469 0.035 1.2 0.017
Bacillus subtilis
ATCC 6633 0.12 1.2 0.058
" (strain ZO 5 A, Fac. Phie)
0.12 1.5 0.044
" (strain 3 R 9575, Merck - ATCC 9524)
0.12 1.8 0.052
Bacillus cereus
ATCC 6630 0.24 2.2 0.084
Bacillus brevis
ATCC 8185 0.14 1.4 0.083
Bacillus mycoides 0.14 1.8 0.049
Bacillus megatherium (NRRL B 1125)
0.25 1.3 0.15
Bacillus polymyxa (NCTC 4747) 0.70 4.4 0.83
Mycobacterium smegmatis - ATCC 607
0.13 1.2 0.21
Mycobacterium phlei (Bacteriological Institute of Lyon)
0.041 5 0.035
Mycobacterium para-smegmatis (A 75 - Lausanne)
0.069 2.2 0.09
Escherichia coli - ATCC 9637 >4.3 500 5.1
Shigella dysenteriae (Shiga L. - Institut Pasteur)
16 2000 13
Salmonella typhimurium (Institut Pasteur)
31 1000 13
Salmonella paratyphi A (Lacasse, Institut Pasteur)
3.9 16
Salmonella schottmuelleri (paratyphi B) (Fougenc,
16 1000 13
Institut Pasteur)
Bacillus lactis aerogenes (Fac. Phie)
1.9 120
Aerobacter aerogenes - ATCC 8308
7.8 1000 6.3
Alcaligenes faecalis - ATCC 8749
0.18 1.8 0.065
Proteus vulgaris (Fac. Phie) 16 >2000 25
Proteus X 19 3.9 62 3.1
Klebsiella pneumoniae - ATCC 10,031
1 8.9 0.88
Serratia marcescens (A. 476,Lausanne)
7.8 120 6.3
Pseudomonas aeruginosa (Bass strain - Institut Pasteur)
16 1000 12
Brucella bronchiseptica (CN 387 - Wellcome Institute)
62 6.3
Pasteurella multocida (A. 125 - Institut Pasteur)
0.24 1.8 0.07
__________________________________________________________________________
These results show that the bacteriostatic activity of 9865 RP, 13057 RP daunorubicin and 13213 RP is exerted against numerous bacteria, certain of which are resistant to one or more of the following antibiotics: penicillin, tetracycline, streptomycin, streptothricin, neomycin, congocidin, erythromycin, carbomycin, spiramycin, streptogramin, chloramphenicol, novobiocin, and the anticancer antibiotics, actinomycin and rufochromomycin. The anticancer activities of 9865 RP and of its three constituents have been demonstrated in the laboratory, where they have been shown to be particularly active against transplantable tumours in the mouse, such as Ehrlich's ascitic tumour, sarcoma 180, benzopyrene saroma and lymphoblastic leucaemia AKR. The most interesting of the new antibiotics in this respect has been shown to be 13057 RP daunorubicin, which shows in the mouse an acute 50% lethal dose (or LD50), determined for subcutaneous administration, of LD50 = 47 mg./kg. s.c. and a subacute 50% lethal dose (or LD50) (giving one dose per day for 5 days), determined for intravenous or subcutaneous administration, of LD50 = 8.75 mg./kg. (intravenously) or LD50 = 13.65 mg./kg. (subcutaneously).
The microorganisms which produce 9865 RP belong to the genus Streptomyces and are designated herein Streptomyces 8899 and Streptomyces 31723 respectively. They have been deposited at the Northern Regional Reseach Laboratory of Peoria, Ill., under the respective references NRRL 3046 and NRRL 3045. Subcultures of either of the said microorganisms can be obtained from the said depository by anyone freely and without restriction. The microorganisms were isolated from soil samples taken in two different regions of Algeria.
The method of isolation was as follows. The soil sample is suspended in sterile distilled water and the suspension diluted to various concentrations. A small volume of each dilution is spread on the surface of Petri dishes containing a nutritive agar medium. After incubation for several days at 26° C. the colonies of microorganisms which it is wished to isolate are pricked out onto agar slopes to give more abundant cultures.
According to the modern classifications designed for the identification of Streptomyces "S. A. Waksman, "The Actinomycetes," The Williams and Wilkins Company, Baltimore, 1961, Vol. II - "Bergey's Manual of Determinative Bacteriology", 7th Edition, The Williams and Wilkins Company, Baltimore, 1957 - L. Ettlinger et coll., Archiv. fur Mikrobiologie, 31, 326 (1958)] no description of any species has been found, the culture characteristics of which coincide with those of Streptomyces 8899 or 31723.
By means of the classification given by G. F. Gause et coll. ("Zur Klassifizierung der Actinomyceten", Veb Gustav Fisher Verlag, Jena, 1958) the species Streptomyces coeruleorubidus has nevertheless been observed as having a description closely similar to that of the newly discovered strains. Although, according to S. A. Waksman (loc.cit. pp. 323-326) this description is somewhat imprecise, it is nevertheless possible to assimilate Streptomyces 8899 and Streptomyces 31723 into the species Streptomyces coeruleorubidus and to list them under the designations Streptomyces coeruleorubidus strain 8899 and Streptomyces coeruleorubidus strain 31723 respectively. In order to clarify their similarities and ddifferences, the detailed characteristics of the two strains Streptomyces 8899 and Streptomyces 31723 are given below parallel with the characteristics of Streptomyces coeruleorubidus as described by G. F. Gause et coll.
The sporulation of Streptomyces 8899 and 31723 is difficult to observe because of its complexity. It is observable either on "synthetic" media such as that described by Grundy et coll. (Antibiotics and Chemotherapy, 1, 309 (1951)) or on complex media such as Benett's medium (K. L. Jones, J. Bacteriol., 57, 142 (1949)). Cultures on thin plates examined under the microscope show the formation of branched filaments and of spore chains characteristic of the genus Streptomyces. The spore-bearing filaments presenting the most complex degree of development are in the form of spirals with serrated coils of several, and often more than five, turns. The spores are oval, measuring about 0.6 - 0.9 to 0.8 - 1.2 μ.
The attachment of the spore-bearing filaments presents a verticillated structure, sometimes monoverticillated but more often biverticillated. This structure is only observable under the microscope if the spore-bearing filaments are only spirals of one or two turns or are reduced to a loop; otherwise the development of spirals is too thick and masks their attachment, hindering the observation of any secondary whorls in their structures.
Taking into account the morphological elements which show the most coplex development, it can be concluded that the spore-bearing apparatus of Streptomyces 8899 and 31723 corresponds to the Biverticillus-spira type described in the classification of T. G. Pridham et coll. [Applied Microbiol., 6, 52 (1958)].
Since the aerial mycelium of well-developed cultures of both of the new types of Streptomyces is light blue, on comparison with Pridham's classification by series, Streptomyces 8899 and 31723 are placed in the Biverticillus-spira blue series section, in which no species are described, though Streptomyces coeruleorubidus appears in the Spira blue series section.
On "synthetic" media, Streptomyces 8899 and 31723 generally possess a vegetative mycelium which is usually rose or orange-rose at the beginning of development, the red colour intensifying with the incubation, becoming also bright red. On "organic" media, the vegetative cycelium is yellow-brown or red-brown. The aerial mycelium is generally well-developed on both types of medium. It is white at the beginning of its development and then rapidly becomes a shade of light blue, called below turquoise blue. According to the degree of development or the nature of the medium, it presents a slightly variable intensity of tone, or its colour may be slightly softened. Pure red or orange-red soluble pigments are formed in synthetic media of intensity which varies with the age of the cultures; the pigment is a softened red (red-brown or rose-brown) in organic media. On Williams and McCoy medium, an abundant production of characteristic black melanic pigment is observed.
The culture characteristics and biochemical properties of Streptomyces 8899 and 31723 have been studied on the usual nutritive agar or liquid media used in the identification of strains of Streptomyces. The observations are given in detail in Table VII; they relate to cultures incubated at 26° C. for about 1 month. The final state of the cultures and the colours produced are given. The references or composition of the culture media are given below. The description of S. coeruleorubidus by G. F. Gause et coll. is given in this Table so far as possible for comparison with cultures obtained on media of similar formulae.
TABLE VII
__________________________________________________________________________
Streptomyces 8899
Streptomyces 31723
Streptomyces
__________________________________________________________________________
coeruleorubidus
Czapeck's agar
Vegetative mycelium:
Vegetative mycelium: slight,
Synthetic medium No. 1 of
(with sucrose)
slight, flat, rose, under-
cracked, yellowish-rose,
Grause et coll.
(ref. 1, medium
side bright red. underside becoming medium red.
Vegetative mycelium: rasp-
No. 1) Aerial mycelium: Aerial mycelium: berry-red to grey-brown.
torquoise blue. turquoise blue. Aerial mycelium: bluish.
Soluble pigment: light red.
Soluble pigment: medium red.
Soluble pigment:
raspberry-
red to grey-brown.
Czapek's agar
Vegetative mycelium: slight,
Vegetative mycelium: slight,
(with glucose)
folded, crackled, rose,
cracked, yellowish-rose,
(ref. 1-A) underside orange-red.
underside becoming medium red.
Aerial mycelium: turquoise
Aerial mycelium: turquoise
blue. blue.
Soluble pigment: red tinged
Soluble pigment: medium red.
with orange.
Agar with calcium
Vegetative mycelium: slight,
Vegetative mycelium: slight,
malate flat, underside pale rose.
flat, underside pale mauve.
(ref. 2) Aerial mycelium: turquoise
Aerial mycelium: rather poorly
blue. developed, white to turquoise
Soluble pigment: pale rose.
blue.
Remark: complete solubili-
Soluble pigment: rose-mauve.
sation of calcium malate in
Remark: complete solubilisa-
one month. tion of calcium malate in
one month.
Agar with tyro-
Vegetative mycelium:
Vegetative mycelium: fairly
sine slight, folded, brown-
thick, folded, very dark
(ref. 3) black. brown.
Aerial mycelium: in traces,
Aerial mycelium: none.
greyish-white. Soluble pigment: dark brown.
Soluble pigment: dark brown.
Remark: no solubilisation of
Remark: no solubilisation of
the tyrosine.
the tyrosine.
Agar with Vegetative mycelium: thick,
Vegetative mycelium: thick,
Vegetative mycelium:
colour-
starch little folded, yellowish-
finely folded, underside
less or rose.
(ref. 1, rose, underside pale rose
dull red.
medium No. 10)
mauve.
Aerial mycelium: turquoise
Aerial mycelium: turquoise
Aerial mycelium: whitish-
blue. blue. bluish.
Soluble pigment: rose
Soluble pigment: rose
Soluble pigment: none. No
tinged with orange.
tinged with orange.
hydrolysis or slow
hydrolysis
of the starch.
Agar with Vegetative mycelium: finely
Vegetative mycelium: slight
(Organic medium No. 2 of
Gause
glucose folded, fluted, underside
and very finely folded,
et coll.)
(ref. 1, light yellow-brown.
yellowish-red then reddish-
Vegetative mycelium:
reddish-
medium No. 7)
Aerial mycelium: poorly
brown. brown.
developed, white to
Aerial mycelium: traces,
Aerial mycelium: sparse,
turquoise blue. white. whitish.
Soluble pigment: yellow-
Soluble pigment: light
Soluble pigment: reddish-
brown to light red-brown.
yellowish-brown. brown.
Asparagine- Vegetative mycelium: slight,
Vegetative mycelium: fairly
glycerine agar
little folded, pale rose
thick and folded, light
(ref. 1, tinged with orange, under-
rose, underside red tinged
medium No. 3)
side rose tinged with orange.
with orange.
Aerial mycelium: turquoise
Aerial mycelium: turquoise
blue. blue.
Soluble pigment: pale rose
Soluble pigment: pale rose
tinged with orange.
tinged with orange.
Benett's agar
Vegetative mycelium: fairly
Vegetative mycelium: slight
(ref. 4) thick, finely folded,
and very finely folded,
light red-brown, underside
shrimp-red, underside
dark brown. reddish-brown.
Aerial mycelium: turquoise
Aerial mycelium: turquoise
blue. blue.
Soluble pigment: red-brown.
Soluble pigment: weak,
Starch-ammonium
Vegetative mycelium: slight,
Vegetative mycelium: slight,
phosphate agar
flat, underside pale
flat, colourless, underside
(ref. 5) yellowish to nearly blue.
slightly rose tinted.
Aerial mycelium: very well
Aerial mycelium: very well
developed, turquoise blue.
developed, turquoise blue.
Soluble pigment: none.
Soluble pigment: none.
Maltose-tryptone
Vegetative mycelium: very
Vegetative mycelium: thick,
agar thick, folded, crackled,
folded, crackled, underside
(ref. 6) underside black-brown.
black-brown.
Aerial mycelium: very well
Aerial mycelium: very well
developed, turquoise blue
developed, turquoise blue
to grey blue. to grey blue.
Soluble pigment: melanic
Soluble pigment: melanic
pigment, intense black-
pigment, intense black-
brown, characteristic.
brown, characteristic.
Gelatine Vegetative mycelium: slight
Vegetative mycelium: pellicle
Vegetative mycelium: dark
(stab culture)
pellicle with yellowish-
fragmented with yellowish-
yellow or grey-brown.
(7) underside. rose underside.
Aerial mycelium: poorly
Aerial mycelium: poorly
Soluble pigment:
grey-brown.
developed, remaining white.
developed, white.
Soluble pigment: medium
Soluble pigment: yellow-
Remark: slow and complete
brown. brown, not abundant.
liquefaction of the
gelatine.
Remark: slow and incomplete
Remark: slow and incomplete
liquefaction of the gelatine.
liquefaction of the gelatine.
Potato Vegetative mycelium: thick,
Vegatative mycelium: thick
Vegetative mycelium:
smooth,
(ref. 1, finely folded, light yellow-
and folded, red tinged with
colourless, yellowish or
dark
medium No. 27)
brown then reddish-brown.
orange to reddish brown.
rose.
Aerial mycelium: turquoise
Aerial mycelium: turquoise
Aerial mycelium:
white-blue,
blue. blue. blue or green-blue; some
Soluble pigment: dark red-
Soluble pigment: dark red-
strains rose-blue.
brown. brown. Soluble pigment: sometimes
dark rose.
Skimmed milk
Vegetative mycelium: thick,
Vegetative mycelium:
Vegetative mycelium:
colour-
(ref. 8) dark yellowish-brown ring.
slight yellowish-rose to
less or yellowish.
reddish-brown ring.
Aerial mycelium: traces,
Aerial mycelium: traces,
Soluble pigment:
grey-brown.
white. white.
Soluble pigment: brown.
Soluble pigment: brown.
Remarks: coagulation and
Remarks: neither coagula-
Remarks: neither coagula-
peptonisation negative or
tion nor peptonisation,
tion nor peptonisation,
positive according to
strain.
change in pH very slight,
weak acidification of
from 6.3-6.5 to 6.0-6.3.
medium as with S. 8899.
Starch solution
Vegetative mycelium: slight
Vegetative mycelium: slight
(ref. 1, pellicle, bright red.
pellicle, bright red.
medium No. 19)
Aerial mycelium: poorly
Aerial mycelium: traces,
developed, white to
white.
turquoise blue.
Soluble pigment: red tinged
Soluble pigment: red tinged
with orange. with orange.
Remark: hydrolysis of the
Remark: hydrolysis of the
starch complete in one
starch complete in one
month. month.
Synthetic solu-
Vegetative mycelium: poorly
Vegetative mycelium: several
Vegetative mycelium:
colour-
tion with developed, slight colour-
isolated, yellowish
less.
nitrate less pellicle. colonies.
(ref. 7) Aerial mycelium: none.
Aerial mycelium: none.
Soluble pigment: sometimes
Soluble pigment: none.
Soluble pigment: none.
yellow.
Remark: no reduction to
Remark: no reduction to
Remarks: reduction
positive
nitrite. nitrite. or negative according to
strain.
Microscopic Spore-bearing filaments in
As Streptomyces 8899.
Spirals of 5-7 turns,
morphology the form of spirals spherical spores.
medium: refs.
arranged in a secondary
4 and 5. verticillate structure.
Spores short ovals.
__________________________________________________________________________
1. S. A. Waksman; "The Actinomycetes", Chronica Botanica Company, Waltham (Mass.), U.S.A., 1950, pages 193-197.
1-A. Obtained by replacing sucrose by the same weight of glucose in the preceeding formula
2. Calcium malate 1%, ammonium chloride 0.5%, dipotassium phosphate 0.05%, agar 2%.
3. Peptone 0.5%, meat extract 0.3%, tyrosine 0.5%, agar 2%.
4. K. L. Jones, J. Bacteriology, 57, 142 (1949).
5. Grundy et coll., Antibiotics and Chemotherapy, 1, 309 (1951).
6. A. M. Williams and E. McCoy, Appl. Microbiol., 1, 307 (1953).
7. Manual of Methods for pure culture study of bacteria, Society of American bacteriologists (II 50 - 18).
8. Commercial skimmed milk powder, reconstituted according to the manufacturers' instructions.
[According to the method of T. G. Pridham and D. Gottlieb, J. Bact. 56, 467 (1946)]
The cultures are carried out on agar slopes at 26° C. Amongst substances regularly giving rise to a rapid and complete growth are: xylose, arabinose, rhamnose, glucose, galactose, mannose, lactose, maltose, raffinose, dextrin, starch, glycerol (in S. 8899 only), adonitol, mannitol, sorbitol, inositol (in S. 8899 only). In contrast, sorbose, inulin (in S. 31723 only), esculin, erythritol and dulcitol allow no development, or only very restricted development. Finally, substances which produce an irregular, moderate or weak growth in the experiments include ribose, levulose, sucrose, inulin (in S. 8899 only), glycerol (in S. 31723 only), and inositol (in S. 31723 only).
The characteristics to be taken into consideration for the systematic classification of S. coeruleorubidus strains 8899 and 31723 are: the turquoise blue colour of the aerial mycelium; the biverticillate structure of the spirals of the spore-bearing apparatus; the positive melamine reaction of cultures on appropriate media; the particular red colour of the vegetative mycelium on appropriate media; and the particular red colour of soluble pigments on appropriate media.
The first two characteristics place S. coeruleorubidus strains 8899 and 31723 in the biverticillus-spira blue series section of Pridham's classification, in which no other species is described. The properties taken together place S. coeruleorubidus strains 8899 and 31723, in the new classification of S. A. Waksman "The Actinomycetes" (The Williams and Wilkins Company, Baltimore, 1961), Vol. II, page 155, in the melamine + group, series 5 (red to reddish-orange growth); no species occurs in this series having a blue aerial mycelium. S. coeruleorubidus strains 8899 and 31723 may therefore be placed in this series with the qualification "blue aerial mycelium".
The process of the invention for the production of antibiotic 9865 RP comprises cultivating Streptomyces 8899 or Streptomyces 31723 or a productive mutant thereof in a nutrient medium containing assimilable sources of carbon, nitrogen, and mineral salts until substantial antibiotic activity is produced by the said microorganism in the said medium, and recovering the said antibiotic from the medium. The culture of Streptomyces 8899 or Streptomyces 31723 may be carried out by any method of aerobic surface or submerged culture, but the latter is preferred for reasons of convenience. For this purpose the various types of apparatus currently used in the fermentaion industry are employed.
The following scheme for making a production culture is preferably used:
______________________________________ Streptomyces 8899 (or Streptomyces 31723) stock ↓ culture on agar ↓ culture in agitated flask ↓ inoculum culture in fermentation vessel ↓ production culture in fermentation vessel ______________________________________
The fermentation medium must contain assimilable sources of carbon, nitrogen, and mineral salts and, optionally, growth factors, all these elements being introduced in the form of well-defined substances or as complex mixtures, such as those encountered in biological products of various origins.
Carbohydrates, such as glucose, lactose, sucrose, molasses; dextrins starch, and other carbohydrates such as the sugar alcohols, e.g. mannitol, may be used as carbon sources, and also certain organic acids, e.g. lactic, citric, and tartaric acids. Certain animal or vegetable oils such as lard or soya oil may advantageously replace these various carbon sources, or be combined with them. A wide range of sources of assimilable nitrogen are suitable. They may be simple chemical substances such as nitrates, inorganic and organic ammonium salts, urea and amino acids. They may also be complex substances containing nitrgoen principally in the form of protein, such as casein, lactalbumin, gluten and hydrolysates therof, soya-, groundnut-, and fish-meals, meat extracts, yeast, distillers' solubles and corn-steep. Amongst the mineral elements added, certain may exert a buffering or neutralising effect, such as alkali metal or alkaline earth metal phosphates and calcium and magnesium carbonates. Other mineral salts contribute to the ionic equilibrium necessary for the development of Streptomyces 8899 and 31723 and the formation of the antibiotic, for example alkali metal and alkaline earth metal chlorides and sulphates. In addition, certain substances act as activators of the metabolic reaction of Streptomyces 8899 and 31723; these are the salts of zinc, cobalt, iron, copper and manganese.
The pH of the nutrient medium at the beginning of culture should be between 6.0 and 7.8, and preferably 6.5 to 7.5. The optimal temperature for the culture is 25°-28° C., but satisfactory production is obtained at temperatures between 23° and 35° C. The aeration of the fermentation medium may b varied over a fairly wide range of values but it has been found that aeration rates of 0.3 to 2 liters of air per minutes per liter of medium are particularly suitable. The maximal yield of antibiotic is obtained after 2 to 5 days of culture, this period depending essentially on the medium used. From the foregoing it will be appreciated that the general conditions for the culture of Streptomyces 8899 and 31723 for the production of antibiotic 9865 RP may be varied to a fairly wide degree.
9865 RP may be isolated from the fermentation cultures by various methods. The fermentation culture may be filtered at a pH between 1.5 and 9 and, in these conditions, the major part of the active material passes into the filtrate. After washing with water, the filter-cake retains practically no active material. It is advantageous to carry out this operation using an acid medium, and particularly one acidified with oxalic acid to a pH between 1.5 and 2. It is also possible to carry out the filtration at a pH between 2 and 7, preferably near to 2, in the presence of an aliphatic alcohol containing 1 to 3 carbon atoms.
In these extraction operations 9865 RP is obtained in aqueous or aqueous-alcoholic solution and it is then extracted with a water-immiscible organic solvent such as butanol, methyl isobutyl ketone, ethyl acetate or chloroform, at a pH between 5.5 and 9, preferably about 7.5. This extraction may be preceded by absorption of the antibiotic on an ion-exchange resin, in which case the aqueous solution is adjusted to a pH about 4 and then treated with a cationic carboxylic exchange resin, preferably Amberlite IRC 50, in the hydrogen form. Elution is then effected with a saline or acidic, aqueous-alcoholic solution, preferably with methanol containing 10% water and 1% sodium chloride. The eluate is concentrated to remove the alcohol and then extracted as described above.
The fermentation medium may also be directly extracted with a water-immiscible organic solvent such as butanol, ethyl acetate or chloroform, at a pH between 5.5 and 9, preferably about 7.5. In this case, all the active material passes into the organic phase, which is separated from the aqueous phase by the usual methods.
Whatever the mode of extraction chosen, the antibiotic 9865 RP is finally obtained in organic solution. It may be advantageous at this stage to purify the antibiotic by successively passing it into aqueous solution and into organic solution by varying the pH. The crude antibiotic may then be isolated from the organic solution obtained in the last-mentioned operation by concentration or precipitation with a poor solvent for the antibiotic, such as hexane. A method of isolation which has been found to be particularly advantageous consists of acidifying the organic solution to a pH of about 4, preferably with acetic acid, and concentrating it under reduced pressure to a smaller volume. Addition of a poor solvent for 9865 RP, such as hexane, to the concentrate obtained causes the precipitation of the crude antibiotic.
To obtain 9865 RP in a purer state, all the usual methods may be used, such as chromatography on an adsorbent substance, countercurrent distribution, or partition between various solvents. It has been found particularly advantageous to utilise one of the following two methods:
chromatography on alumina at pH 4 of the crude antibiotic dissolved in butanol; and solution of the crude antibiotic in a mixture of methylene chloride-carbon tetrachoride-water (5:1:6 by volume), decantation of the aqueous phase followed by its extraction with methylene chloride, combination of the methylene chloride extracts, and concentration of the latter under reduced pressure, followed by the addition of hexane to the concentrate obtained to precipitate the purified antibiotic. A similar method may also be used in which the methylene chloride is replaced by ethyl acetate.
It is possible to repeat the differnt methods indicated for the extraction and isolation of 9865 RP several times according to manufacturing requirements, to obtain this antibiotic in a form pure enough for the purposes envisaged.
The 9865 RP isolated by any of the foregoing methods may then be separated into its three constituents, 13057 RP daunorubicin, 13213 RP and 13330 RP. This separation may be effected by the usual methods used for the separation of an antibiotic into its constituents, such as chromatography on various substances or countercurrent distribution. It has been found that the latter gives the more advantageous results, in particular when carried out by one of the following processes, which are, however, only preferred procedures: to obtain 13057 RP daunorubicin alone, countercurrent distribution of 9865 RP with a butanol-phosphate-buffer of pH 7-7.5 system; to obtain 13213 RP alone, countercurrent distribution of 9865 RP in a butanol-ethyl acetate system buffered to pH 4; and to obtain the separation of the three constituents from 9865 RP, two successive countercurrent distributions, at first with a limited number of transfers with a system composed of two chlorinated aliphatic hydrocarbons buffered to pH 5.8, which produces two fractions, an aqueous phase containing 13057 RP daunorubicin contaminated with 13213 RP and an organic phase containing a mixture of 13213 RP and 13330 RP contaminated with 13057 RP daunorubicin, followed by the separate treatment of the two fractions thus obtained with an ethyl acetate-methanol system phosphate-buffered to pH 5.5, which permits, on the one hand, the isolation of 13057 RP daunorubicin and, on the other, the separation of 13213 RP and 13330 RP.
The various countercurrent distribution operations may be preceded or followed by the usual purification processes, particularly extraction or recrystallisation, in order to obtain the three constituents in a form pure enough for the use envisaged.
The following non-limitative Examples illustrate the invention. Activity is throughout determined by turbidimetric estimation, using Klebsiella pneumoniae as the sensitive organism, by comparison with a sample of 9865 RP of known activity used as control. This activity is expressed in units (u) per mg. for solid products and in units per cc. for solution. (The unit is defined as the smallest quantity of product which, dissolved in 1 cc. of an appropriate medium, inhibits the growth of Klebsiella pneumoniae under the conditions in question).
A 170 liter fermentation vessel is charged with:
______________________________________ Corn steep 2.400 kg. Sucrose 3.600 kg. Calcium carbonate 0.900 kg. Ammonium sulphate 0.240 kg. Water to 100 liters. ______________________________________
This culture medium has a pH of 6.15. It is sterilised by passage of steam at 122° C. for 40 minutes. After cooling, the volume of the broth is 120 liters and the pH is 7.20. The medium is then seeded with 200 cc. of a culture in an agitated Erlenmeyer flask of the strain Streptomyces 31723. The culture is carried out for 27 hours at 26°-27° C. with agitation and aeration with sterile air. It is then suitable for seeding the production culture.
The production culture is carried out in an 800 liter formentation vessel charged with the following:
______________________________________
Soya flour 20 kg.
Distillers' solubles
2.500 kg.
Starch 10 kg.
Soya oil 2.500 liters
Sodium chloride 5 kg.
Water to 465 liters.
______________________________________
The pH of the medium thus obtained is adjusted to 7.20 with concentrated sodium hydroxide solution (400 cc.). The medium is then sterilised by the passage of steam at 122° C. for 40 minutes. After cooling, the volume of the broth is 500 liters and the pH is 6.75. It is then seeded with 50 liters of the culture from the 170 liter fermentation vessel. Culture is carried out at 28° C. for 67 hours with agitation and aeration with sterile air. The pH of the medium is then 7.40 and the volume of the fermentation culture is 520 liters. The quantitiy of antibiotic present in the medium is 29 μ/cc.
An inoculum culture is carried out in a 170 liter fermentation vessel under the same conditions as in Example 1 but seeding with 200 cc. of a culture in an agitated Erlenmeyer flask of the strain Streptomyces 8899.
The production culture is then carried out in an 800 liter fermentation vessel charged with the medium described in Example 1. The pH of the medium is adjusted to 8.10 with concentrated sodium hydroxide solution (750 cc.), and the medium is then sterilised by the passage of steam at 122° C. for 40 minutes. After cooling, the volume of the broth is 500 liters and the pH 6.80. The medium is then seeded with 75 liters of the culture in the 170 liter fermentation vessel, and the culture is carried out at 26°-27° C. for 67 hours with agitation and aeration with sterile air. The pH of the medium is then 7.40 and the volume of the fermentation culture is 545 liters. The quantity of antibiotic present in the medium is 9.1 μ/cc.
The fermentation culture from Example 1 (520 liters: activity 29 μ/cc.) is placed in a vessel equipped with an agitator and the pH is adjusted to 1.8 with a concentrated solution of oxalic acid. Agitation is carried out for one hour and a filtration adjuvant (20 kg.) then added. The mixture is filtered on a filter-press and the filter-cake washed with water (100 liters) acidified to pH 2 with oxalic acid. The filtrate (612 liters) is treated with concentrated sodium hydroxide solution until the pH is 4.5. The filtrate is then passed through a column containing Amberlite IRC 50 in hydrogen form (20 liters: diameter of column 15.2 cm., height of column 200 cm., height of resin at rest in column 110 cm.). The filtrate passes through the bed of Amberlite from base to top at a rate of 40 liters/hour. The column is then washed with water (100 liters) at a rate of 50 liters/hour circulating from base to top and then with methanol (containing 10% water; 75 liters) circulating from top to base at a rate of 50 liters/hour. The washings are discarded and the column is then eluted with a solution having the following composition (per liter):
______________________________________ sodium chloride 10 g. water 100 cc. methanol to 1000 cc. ______________________________________
The eluate (100 liters), which contains the major part of the antibiotic, is concentrated under reduced pressure at 35° C. to 10 liters. The concentrate is extracted at pH 7.5 with chloroform (2 × 5 liters). The chloroformic extract is adjusted to pH 4 with a solution of acetic acid in chloroform (10:100 by volume) and then concentrated at 30° C. under reduced pressure to 100 cc. The antibiotic is precipitated by the addition of hexane (1 liter), separated, washed and dried to give an amorphous red powder (9 g.) of activity 1,400 μ/mg.
The crude antibiotic (17.1 g.) obtained as described in Example 3 (activity 1530 μ/mg.) is dissolved with stirring in a mixture of methylene chloride (1.5 liters), carbon tetrachloride (0.3 liters) and water (1.8 liters). The pH is then adjusted to 3 by the addition of normal hydrochloric acid (8 cc.). After decanting, the aqueous phase is treated with methylene chloride (7 liters) and 0.1N sodium hydroxide solution (200 cc.) to give a pH of 7.5. After decanting, the aqueous phase is again extracted at pH 7.5 with methylene chloride (3.5 liters). The methylene chloride extracts are combined and concentrated to 100 cc. After the addition of hexane (1 liter) to the concentrate, a product precipitates which is filtered off, washed and dried at 30° C. under reduced pressure to give the antibiotic 9865 RP (9.15 g.) in the form of an amorphous orange-red powder of activity 2180 μ/mg.
A mixture is prepared of methylene chloride, carbon tetrachloride and MacIlvaine buffer - pH 5.8 (20 cc. of this buffer are prepared by the addition of 12.09 cc. of 0.2 M Na2 HPO4 solution to 7.91 cc. of 0.1 M citric acid solution) in the proportions 2:1:3 (by volume). When this mixture is in equilibrium, the two phases are separated. 9865 RP (10 g.) of activity 1750 μ/mg. (obtained as described in Example 4) is dissolved in a mixture of the phases (1 liter of each). This system is subjected to a countercurrent distribution of 6 transfers in 5 liter cells, using the heavy (organic solvent) phase as the mobile phase and the light (aqueous) phase as the stationary phase and using 1 liter of each phase each time. The mixtures of lower phases (mixture A) and upper phases (mixture B) of the first 4 cells, and the mixtures of lower phases (mixture C) and upper phases (mixture D) of the last 3 cells, are collected separately.
Mixture B is adjusted to pH 7.5 by the addition of normal sodium hydroxide solution (300 cc.) and then extracted with chloroform (4 liters, 2 liters and 1 liter). The chloroformic extracts and mixture A are combined and concentrated under reduced pressure (to 700 cc.). The concentrate is washed with water at pH 7.5 (2 × 350 cc.) and the mother liquors of the washings are extracted with chloroform (2 × 100 cc.). The washed concentrate and the chloroformic extracts are combined and concentrated under reduced pressure to 70 cc. Hexane (700 cc.) is then added and the precipitate produced is filtered off, washed and dried under reduced pressure at 30° C., giving a fraction F1 (5.1 g.) containing principally the antibiotic 13057 RP daunorubicin.
In a separate operation, mixture D is extracted with methylene chloride (3 liters and 1.5 liters). The methylene chloride extracts and mixture C are combined and concentrated under reduced pressure to 800 cc. The concentrate is washed with water (400 cc.) and then concentrated again to 700 cc. Hexane (1 liter) is added and the precipitate produced is filtered off, washed and dried under reduced pressure at 30° C., to give a fraction F2 (3.7 g.) containing principally 13213 RP and 13330 RP.
A product (10 g.), similar to fraction F1 mentioned above, is subjected, after dissolved in an ethyl acetate-methanol - pH 5.5 M/15 phosphate buffer system (8:3:5 by volume; 200 cc.), to a countercurrent distribution of 110 transfers in a 50 cell Craig apparatus (50 transfers in the apparatus and 60 transfers by the "single withdrawal" technique) beginning at the first two cells. The mixture of the upper phases of cells 0 to 37 (3.8 liters) is recovered and concentrated to 300 cc.) The concentrate thus obtained and the mixture of the lower phases of cells 0 to 37 (3.8 liters) are then combined and concentrated to 800 cc. The pH is adjusted to 8 by the addition of normal sodium hydroxide solution (180 cc.) and the solution obtained is extracted with chloroform (800 cc. and 400 cc.). The chloroformic extracts are concentrated to 400 cc. and washed with water (400 cc.) made alkaline to pH 8. The mother liquors of the washing are extracted with chloroform (200 cc.). The washed concentrate and the chloroformic extracts are combined, concentrated to 400 cc., washed with water (400 cc.) made alkaline to pH 8, and concentrated to 100 cc. Butanol (200 cc.) is added, and the mixture concentrated to 100 cc. The butanolic solution obtained is adjusted to pH 3.5 by the addition of butanol saturated with normal hydrochloric acid (30 cc.) and kept for 12 hours at 4° C. Crystals form which are filtered off, washed and dried, giving a first crop (4.55 g.) of crude 13057 RP daunorubicin hydrochloride. Concentration to 100 cc. of the crystallisation mother liquors, addition of hexane (1 liter) and filtering, washing and drying the precipitate produced, gives a second crop (2.5 g.) of crude 13057 RP daunorubicin hydrochloride.
Crude 13057 RP daunorubicin hydrochloride (3.75 g.), obtained as described in Example 6, is dissolved in dioxan (40 cc.) containing 20% water. The solution obtained is filtered and anhydrous dioxan (15 cc.) is added over 2 hours, followed by anhydrous dioxan (235 cc.) over 30 minutes. A product crystallises which is separated, washed and dried, giving 13057 RP daunorubicin hydrochloride (2.75 g.) in the form of orange-red needles, m.p. 225°-230° C. (with decommposition), of activity 151 μ/mg.
This compound (0.208 g.) is dissolved in a mixture of water (200 cc.) and butanol (150 cc.). 0.1N sodium hydroxide solution (3.4 cc.) is added, the mixture is separated and the aqueous phase then extracted with butanol (50 cc.). The butanolic extracts are combined, washed with water made alkaline to pH 8 (2 × 100 cc.) and concentrated to 10 cc. The concentrate obtained is treated with hexane (50 cc.) and the precipitate producted is filtered off, washed and dried, giving 13057 RP daunorubicin (0.0945 g.) in the form of an amorphous red powder, activity 160 μ/mg.
A product (5 g.), similar to fraction F2 obtained in Example 5, is subjected, after being dissolved in an ethyl acetate-methanol - pH 5.5 M/15 phosphate buffer system (8:3:5 by volume; 200 cc.), to a countercurrent distribution identical with that described in Example 6. The mixture of the upper phases of cells 36 to 89 (5.3 liters) is recovered and concentrated to 500 cc. The concentrate thus obtained and the mixture of the lower phases of cells 36 to 89 (5.3 liters) are combined and concentrated to 800 cc. The concentrate is extracted successively with methylene chloride (2 × 800 cc.) and chloroform (800 cc.). The extracts obtained are combined, concentrated to 400 cc., washed with water at pH 7.5 (2 × 400 cc.) and then concentrated to 10 cc. Addition of hexane (100 cc.) causes the precipitation of a product which is filtered off, wahed and dried under reduced pressure, giving 13213 RP (1.1 g.) in the form of an amorphous orange-red powder, activity 2,650 μ/mg.
The fermentation culture (500 liters) obtained in Example 2 is treated as described in Example 3, giving crude 9865 RP (8.5 g.), activity 395 μ/gm. This crude product (17 g.) is purified as described in Example 4 but replacing the methylene chloride by ethyl acetate to give 9865 RP (3 g.), activity 1300 μ/mg.
9865 RP (12.4 g.), obtained as described in Example 9, is subjected, in a butanol - pH 7.35 M/3 phosphate buffer system, to a 50-transfer countercurrent distribution. By extraction with butanol of the lower phases of cells 12 to 35, concentration of the butanolic extracts, washing and the addition of hexane, a first crop (1 g.) of 13057 RP daunorubicin hydrochloride is obtained, followed, after concentration of the mother liquors, by a second crop (1.1 g.) of the same product. These two crops, after recrystallisation from aqueous dioxan, take the form of orange-red needles, m.p. about 225°-230° C. (with decomposition), activity 67 μ/mg.
A similar treatment applied to cells 36 to 49 gives crude 13213 RP (1.1 g.), activity 1800 μ/mg., which, after being subjected to a 50-transfer countercurrent distribution in a butanol-ethyl acetate - pH 4 MacIlvaine buffer sytem (3:7:10 by volume), gives 13213 RP (0.5 g.) in the form of an amorphous orange-red powder, activity 2000 μ/mg.
A fermentation culture (625 liters), prepared as described in Example 2, is placed in an agitated vessel. The pH is adjusted to 9 with concentrated sodium hydroxide solution. Agitation is continued for 30 minutes and a filter-adjuvant (32 kg.) then added. The mixture is filtered on a filter-press and washed with water (275 liters). The filtrate (780 liters) is treated with sodium chloride (156 kg.) and the pH adjusted to 3 with 12N hydrochloric acid. The filtrate is then extracted with butanol (260 liters) and the butanolic extract concentrated under reduced pressure at 35° C. to 4 liters. The concentrate is filtered and the crude antibiotic precipitated from the clarifed solution with petroleum ether (32 liters), separated, washed and dried in vacuo at 30° C., giving crude 9865 RP (227 g.) as a red-brown powder, activity 45 μ/mg.
The crude product (50 g.) obtained is dissolved in butanol saturated with water (200 cc.) and the solution obtained is chromatographed at pH 4 through a column containing alumina (500 cc.). After fixation of the antibiotic, the chromatogram is developed and eluted with butanol saturated with water (4 liters). Three coloured fractions are recovered (respective volumes 450 cc., 1500 cc. and 1500 cc.). The first fraction is concentrated under reduced pressure to 50 cc. and then treated with hexane (500 cc.), giving 9865 RP (8.3 g.), activity 68.5 μ/mg. The second two fractions are each concentrated under reduced pressure to 100 cc. and treated with hexane (1 liter each) to give, respectively, 9865 RP (4.4 g.), activity 216 μ/mg. and 9865 RP (1.35 g.), activity 800 μ/mg.
A fermentation culture (425 liters), prepared as described in Example 1 (activity 40 μ/cc.), is acidified to pH 1.8 with oxalic acid and filtered. The filter-cake is washed with water (100 liters) acidified to pH 2 with oxalic acid and the combined filtrate obtained (500 liters) is extracted at pH 8 with chloroform (150 liters and 100 liters). The extracts are combined and extracted with water at pH 4 (80 liters and 50 liters). The aqueous extract obtained is made alkaline to pH 8 with normal sodium hydroxide solution and extracted with chloroform (40 liters and 20 liters). The chloroformic extracts thus obtained are acidified to pH 4 with a solution of acetic acid in chloroform (10:100 by volume) and the acidified extract concentrated at 30° C. under reduced pressure to 50 cc. The crude antiobiotic is then precipitated by the addition of hexane (500 cc.), separated, washed and dried in vacuo at 30° C., giving 9865 RP (680 mg.) in the form of a red powder, activity 1080 μ/mg.
9865 RP (500 mg.), obtained as described in Example 4, is dissolved in normal sulphuric acid (100 cc.) and the solution obtained is heated for 20 minutes on a water-bath. After cooling and extracting with ethyl acetate (3 × 200 cc.), the organic extract is dried over anhydrous sodium sulphate, filtered and concentrated to a small volume, giving, after filtering, washing and drying, crystals (218.5 mg.). These crystals (150 mg.) are dissolved in chloroform (3 cc.) and benzene (1.5 cc.) and the solution obtained is chromatographed on 20 sheets of Arches No.310 paper impregnated with a solution of acetone containing 20% formamide, and developed for 90 minutes by means of a 2:1 mixture of chloroform and benzene saturatd with formamide. The principal zone of Rf = 0.86 is cut out of each of the 20 sheets and the 20 zones thus cut out are comminuted in a mixer in the presence of methanol. The mixture obtained is filtered, concentrated, and water (10 volumes) added. The precipitate obtained is filtered off, washed and dried under reduced pressure to give crystals (120 mg.). These crystals (170 mg.) are dissolved in dioxan containing 20% water (15 cc.) and water acidified to pH 4 with 0.1N hydrochloric acid is added dropwise. The crystals formed are filtered off, washed and dried, thus giving the aglycone of 9865 RP (130 mg.) in the form of orange-red needles, having a first melting point at 160° C. and a second at 225°-230° C.
13057 RP daunorubicin (500 mg.), obtained as described in Example 7, is treated with sulphuric acid as described in Example 13 for 9865 RP, giving crystals (300 mg.) which, after being treated as described in Example 13, yield the aglycone of 13057 RP daunorubicin (202 mg.) in the form of orange-red needles having a first melting point at 160° C. and a second at 225°-230° C. This aglycone is identical with that of 9865 RP.
The present invention includes within its scope pharmaceutical compositions containing at least one of the antibiotics defined above is association with a compatible pharmacologically acceptable carrier. The compositions may also contain other physiologically active substances. These compositions may be made up in any pharmaceutical form appropriate for the route of administration in question. Intravenous administration of 13057 RP daunorubicin is preferred.
Solid compositions for oral administration include compressed tablets, pills, dispersible powders, and granules. In such solid composition one or more of the new antibiotics is, or are, admixed with at least one inert diluent such as calcium carbonate, potato starch, alginic acid, or lactose. The compositions may also comprise, as in normal practice, additional substances other than inert diluents. e.g. lubricating agents, such as magnesium stearate. Liquid compositions for oral administration include pharmaceutically acceptable emulsions, solutions, suspensions, syrups and elixirs containing inert diluents commonly used in the art, such as water and liquid paraffin. Besides inert diluents such compositions may also comprise adjuvants, such as wetting and suspending agents, and sweetening, flavouring, perfuming and preserving agents. The compositions according to the invention, for oral administration, also include capsules of absorbable material such as gelatin containing one or more of the new antibiotics with or without the addition of diluents or excipients.
Preparationss according to the invention for parenteral administration include sterile aqueous or non-aqueous solutions, suspensions, or emulsions. Examples of non-aqueous solvents or suspending media are propylene glycol, polyethylene glycol, vegetable oils such as olive oil, and injectable organic esters such as ethyl oleate. These compositions may also contain adjuvants such as preserving, wetting, emulsifying and dispersing agents. They may be sterilised by, for example, filtration through a bacteria-retaining filter, by incorporation in the compositions of sterilising agents, by irradiation, or by heating. They may also be manufactured in the form of sterile solid compositions, which can be dissolved in sterile water or some other sterile injectable medium immediately before use.
The percentage of active ingredient in the compositions of the invention may be varied, it being necessary that it should constitute a proportion such that a suitable dosage for the therapeutic effect desired shall be obtained. Obviously several unit dosage forms may be administered at about the same time. In general, the preparations should normally contain at least 0.001 % by weight of active substance when required for administration by injection. For oral administration the preparations will normally contain at least 0.1 % by weight of active substance.
For the treatment of human cancer of the kinds mentioned above by intravenous administration, daily doses are generally between 0.1 and 2 mg/kg for an adult. Compositions for injection consist, for example, of a solution containing 0.1 mg/cc. of active substance in sterile physiological saline.
In more detail, the manner of using 13057 RP daunorubicin in the treatment of various types of cancer is as follows:
Daunorubicin is essentially intended to obtain a remission. The induction treatment, and the reinduction treatments which may follow it, consist of injections repeated at progressively increasing intervals, spaced over from one to several months, which excludes the use of daunorubicin as a maintenance treatment by itself and for a prolonged period. Daunorubicin exercises a depressant action on the blood-forming centers and its administration is sometimes accompanied by cardiac complications. Daunorubicin cannot be used without frequent and regular blood tests and rigorous cardiological testing, before and during treatment.
Daunorubicin is preferably administered by means of intravenous perfusion. Solutions of daunorubicin must be prepared at the time they are required. This is done, for example, by shaking together in a stoppered vessel 20 mg of dry daunorubicin and the contents of an ampoule (4 cc) of solvent (water for injectable preparations), until the daunorubicin is completely dissolved. The solution prepared in this manner is injected through a catheter as a venous perfusion in 100 or 200 cc of isotonic sodium chloride solution. In order to avoid irritation by the medication of the surrounding tissues and of the vascular linings, it is essential that administration should be strictly intravenous and that the rate of perfusion should be rapid so as to prevent local stasis of the product.
The dosage varies according to the clinical circumstances, the therapeutic response, and the blood picture. Also, the data given hereafter indicate mainly an order of magnitude.
Treatment of acute leukaemias must be intensive and of short duration; depending on the case, it comprises one or more courses. In the lymphoblstic forms of leukaemia, the actual trend is to administer a daily dose of 1 mg/kg body weight of two to eight consecutive days, and to cease injections when the leucopenia reaches 1,000 to 1,500 units per cc. It will be recalled that characteristic changes in the medullary cytology fcilitate the conducting of the treatment and help in its adaptation to each particular case. The appearance of giant lymphoblasts slightly preceding aplasia, indicates that administration of daunorubicin should be suspended. It is, moreover, at the end of the aplastic phase, when the number of leucocytes is rising again, that adjustement of the theraputic dose is difficult. When, the day after medication was stopped the leucopenia worsens and the medullary blasts change, it is required to wait for regeneration of the blood before proceeding with a bone marrow test. If the lqucopenia is not accentuated and the medullary cytology remains high with persistence of blastic cells, a second course is undertaken. When the marrow is poor and blastic, one or two complementary injections at intervals of one or two days are frequently necessary. The overall dosage corresponding to the group of courses making up the initial treatment, such as has just been defined, is far from being uniform; calculated per kg weight, it sometimes reaches 20 mg, a dose of around 25 mg being considered the maximum safe dose. The procedure is identical in acute myeloblastic leukaemias, but the daily dose is increased to 2 mg/kg.
It is also possible to adopt, for the treatment of acute leukaemias in their evolutive stage, a dosage based on the body surface area, and to use a daily dose of 30 mg/sq. meter for 3 to 5 successive days depending on the tolerance. After a minimum lapse of 5 days, a new course of the same duration is carried out; a total of three courses may be undertaken. It is emphasized that the overall dose could not be predicted; it varied in the course of experiments from 100 mg to 350 mg/sq. meter.
In chronic myeloid leukaemias, administration of 2 mg/kg of daunorubicin every 2 or 3 days, with twice-weekly testing of the leukocytosis, has been proposed.
Various schemes of multiple chemotherapy incorporating daunorubicin have been proposed. One such technique involves an initial treatment completed by a reinforcing therapy on which reinduction treatments are grafted. The initial treatment combines daily oral administration of prednisone and weekly intravenous injections, in the form of a perfusion, of daunorubicin and vincristine until complete remission is obtained. Calculated per square meter of body surface, the doses are 100 mg per day of prednisone, 2 mg of vincristine and 60 mg of daunorubicin per week. Fifteen days after remission, a repeat injection of vincristine (2 mg/m2) and daunorubicin (30 mg/m2) is given; then the maintenance treatment is started, combining daily ingestion of 6-mercaptopurine (90 mg/m2) and intramuscular administration, every 7 days, of methotrexate (15 mg/m2). The reinduction treatments intended for the 2nd, 4th, 7th, 11 months, and so on, consist of a twice weekly injection of daunorubicin and vincristine in doses respectively of 30 mg/m2 and 2 mg/m2 per injection, as well as daily absorption of prednisone for 7 days. In addition, methotrexate is administered by spinal injection, at the rate of two injections during each reinduction and one monthly injection in between.
In a procedure designed for acute lymphoblastic leukaemias, 1.5 mg/m2 of vincristine one day of a week, is prescribed; the same day and the day after, 20 mg/m2 of daunorubicin are injected, while prednisone is administered during seven consecutive days at a dose of 100 mg/m2. Depending on the cases, a total of one to six weekly courses have been made. In the presence of acute granulocytic forms, where the number of weekly courses varied from two to three, the dosage of daunorubicin was 20 mg/m2 per day during three consecutive days, in combination with methylglyoxal - bis - guanylhydrazone, at the rate of 100 mg/m2 every other day.
Claims (5)
1. Process for the production of daunorubicin, which comprises cultivating aerobically by the submerged culture technique a microorganism selected from the class consisting of Streptomyces coeruleorubidus, NRRL 3045 and 3046, in a liquid nutrient medium, of initial pH 6.0 to 7.8 and at 23° to 35° C., containing assimilable sources of carbon, nitrogen, and mineral salts with an aeration rate of 0.3 to 2 liters of sterile air per minute per liter of medium until substantial antibiotic activity is produced by the said microorganism in the said medium, recovering an orange-red antibiotic mixture containing daunorubicin from the medium, and isolating daunorubicin from the said orange-red antibiotic mixture.
2. Process as claimed in claim 1 in which the pH of the nutrient medium at the beginning of culture is between 6.5 and 7.5.
3. Process as claimed in claim 1 in which the temperature of the culture is 25°-28° C.
4. Process according to claim 1 in which daunorubicin is isolated from the antibiotic mixture by a distribution process.
5. Process according to claim 4 in which the daunorubicin is isolated by countercurrent distribution.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US04/777,876 US3989598A (en) | 1962-05-18 | 1968-11-21 | Antibiotic daunorubicin and its preparation |
| US05/313,790 US3997663A (en) | 1962-05-18 | 1972-12-11 | Antibiotic daunorubicin and its preparation |
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR62.898076 | 1962-05-18 | ||
| FR898076A FR1533151A (en) | 1962-05-18 | 1962-05-18 | New antibiotic and its preparation |
| US04/280,816 US3997662A (en) | 1962-05-18 | 1963-05-16 | Antibiotics and their preparation |
| US04/777,876 US3989598A (en) | 1962-05-18 | 1968-11-21 | Antibiotic daunorubicin and its preparation |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US04/280,816 Continuation-In-Part US3997662A (en) | 1962-05-18 | 1963-05-16 | Antibiotics and their preparation |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US05/313,790 Continuation US3997663A (en) | 1962-05-18 | 1972-12-11 | Antibiotic daunorubicin and its preparation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3989598A true US3989598A (en) | 1976-11-02 |
Family
ID=27246580
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US04/777,876 Expired - Lifetime US3989598A (en) | 1962-05-18 | 1968-11-21 | Antibiotic daunorubicin and its preparation |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US3989598A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4198480A (en) * | 1976-05-31 | 1980-04-15 | Zaidan Hojin Biseibutsu Kagaku Kenkyu Kai | Process for producing antibiotic baumycin complex and components |
| US4592999A (en) * | 1982-07-24 | 1986-06-03 | Sanraku Incorporated | Process for producing daunomycin |
| DE10158036A1 (en) * | 2001-11-27 | 2004-02-05 | Kosmas Kg | Antiallergic pharmaceutical compositions, useful e.g. for treating allergic rhinitis or asthma, containing lactalbumin hydrolyzate (or its fraction) to improve effectiveness and reduce dose of active agent |
| CN101798328A (en) * | 2010-03-20 | 2010-08-11 | 山东新时代药业有限公司 | Improvement method of extraction and purification technology of daunorubicin fermentation liquor |
| WO2018130679A1 (en) | 2017-01-16 | 2018-07-19 | INSERM (Institut National de la Santé et de la Recherche Médicale) | Methods and pharmaceutical compositions for reducing cd95- mediated cell motility |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB985598A (en) * | 1962-05-18 | 1965-03-10 | Rhone Poulenc Sa | Improvements in or relating to antibiotics and their preparation |
-
1968
- 1968-11-21 US US04/777,876 patent/US3989598A/en not_active Expired - Lifetime
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB985598A (en) * | 1962-05-18 | 1965-03-10 | Rhone Poulenc Sa | Improvements in or relating to antibiotics and their preparation |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4198480A (en) * | 1976-05-31 | 1980-04-15 | Zaidan Hojin Biseibutsu Kagaku Kenkyu Kai | Process for producing antibiotic baumycin complex and components |
| US4592999A (en) * | 1982-07-24 | 1986-06-03 | Sanraku Incorporated | Process for producing daunomycin |
| DE10158036A1 (en) * | 2001-11-27 | 2004-02-05 | Kosmas Kg | Antiallergic pharmaceutical compositions, useful e.g. for treating allergic rhinitis or asthma, containing lactalbumin hydrolyzate (or its fraction) to improve effectiveness and reduce dose of active agent |
| DE10158036B4 (en) * | 2001-11-27 | 2007-05-03 | Kosmas Kg | Antiallergic agent and its use |
| CN101798328A (en) * | 2010-03-20 | 2010-08-11 | 山东新时代药业有限公司 | Improvement method of extraction and purification technology of daunorubicin fermentation liquor |
| CN101798328B (en) * | 2010-03-20 | 2012-05-23 | 山东新时代药业有限公司 | Improvement method of extraction and purification technology of daunorubicin fermentation liquor |
| WO2018130679A1 (en) | 2017-01-16 | 2018-07-19 | INSERM (Institut National de la Santé et de la Recherche Médicale) | Methods and pharmaceutical compositions for reducing cd95- mediated cell motility |
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